US4241701A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method and apparatus for controlling steam temperature at a boiler outlet
Assignee: ICS Triplex Technology Ltd
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Filing: 1979-02-16
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Granted: 1980-12-30
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Expires: 1999-02-16
Abstract
Abstract Boiler outlet temperature in a sliding pressure operation is controlled in a routine way by varying the fluid or heat distribution in the boiler. The effect a change in pressure has on steam temperature is anticipated by supplying a feedforward signal to the temperature control system from drum pressure so as to minimize temperature variations at the boiler outlet.
Inventors
- 👤 Richard H. Morse
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 10:29
CPC Classifications
F; F22; F22G; F22G5/00; F22G5/12
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
116 words
In a drum type boiler having a superheater and a control system for modifying the fluid distribution or the heat distribution in said boiler to control the temperature of the steam at the outlet of said superheater wherein the control system includes a controller responsive to the difference between said outlet temperature and its set point for effecting said modification to control the temperature at said superheater outlet, the improvement which comprises: means for producing a feedforward signal proportional to boiler drum pressure; and means responsive to said feedforward signal for modifying the control of said outlet temperature in sense to prevent the temperature at said superheater outlet from changing in response to drum pressure changes.
Claim 2
Dependent Claim
116 words
In a drum type boiler having a superheater and a control system for modifying the fluid distribution or the heat distribution in said boiler to control the temperature of the steam at the outlet of said superheater wherein the control system includes a controller responsive to the difference between said outlet temperature and its set point for effecting said modification to control the temperature at said superheater outlet, the improvement which comprises: means for producing a feedforward signal proportional to boiler drum pressure; and means responsive to said feedforward signal for modifying the control of said outlet temperature in sense to prevent the temperature at said superheater outlet from changing in response to drum pressure changes.
Claim 3
Dependent Claim
111 words
In a drum type boiler having a superheater and a control system for modifying the operation of said boiler to control the temperature of the steam at the outlet of said superheater wherein the control system includes a controller responsive to the difference between said outlet temperature and its set point for controlling the outlet temperature, the improvement which comprises: means for producing a feedforward signal proportional to the drum pressure in the boiler; and means for applying said feedforward signal to said controller in such sense as to modify the control so as to tend to minimize changes in the temperature at said outlet due solely to drum pressure changes.
Claim 4
Dependent Claim
111 words
In a drum type boiler having a superheater and a control system for modifying the operation of said boiler to control the temperature of the steam at the outlet of said superheater wherein the control system includes a controller responsive to the difference between said outlet temperature and its set point for controlling the outlet temperature, the improvement which comprises: means for producing a feedforward signal proportional to the drum pressure in the boiler; and means for applying said feedforward signal to said controller in such sense as to modify the control so as to tend to minimize changes in the temperature at said outlet due solely to drum pressure changes.
Claim 5
Dependent Claim
156 words
In a drum type boiler having primary and secondary superheater sections with a spray desuperheater between them and a control system for modifying the water flow to the desuperheater to control the temperature of the steam at the outlet of said secondary superheater wherein the control system includes a first controller responsive to the difference between said outlet temperature and its set point for controlling the set point of a second controller which responds to the difference between its set point and the inlet temperature of said secondary superheater, the improvement which comprises: means for applying a feedforward signal to said control system to change the output of said first controller in response to said feedforward signal with the feedforward signal being proportional to the drum pressure in the boiler and the application of said feedforward signal being of sense to minimize the tendency of said secondary superheater outlet to increase when the drum pressure decreases.
Claim 6
Dependent Claim
156 words
In a drum type boiler having primary and secondary superheater sections with a spray desuperheater between them and a control system for modifying the water flow to the desuperheater to control the temperature of the steam at the outlet of said secondary superheater wherein the control system includes a first controller responsive to the difference between said outlet temperature and its set point for controlling the set point of a second controller which responds to the difference between its set point and the inlet temperature of said secondary superheater, the improvement which comprises: means for applying a feedforward signal to said control system to change the output of said first controller in response to said feedforward signal with the feedforward signal being proportional to the drum pressure in the boiler and the application of said feedforward signal being of sense to minimize the tendency of said secondary superheater outlet to increase when the drum pressure decreases.
Claim 7
Dependent Claim
49 words
Apparatus as set forth in claim 3 in which said feedforward signal is applied in attenuated form to the second controller so that the controller operates to control said desuperheater to provide an anticipatory control of the steam temperature which is independent of the action of said first controller.
Claim 8
Independent Claim
112 words
A method for controlling the temperature of the steam at the outlet of the superheater of a drum type boiler operating in the sliding pressure mode, comprising the steps of: automatically controlling the fluid distribution or the heat distribution in the boiler in response to the deviation of outlet temperature from its set point so as to tend to maintain said outlet temperature at its set point; and modifying said control in response to the magnitude of a feedforward signal proportional to the pressure of the steam in said drum, said modification being in sense to tend to reduce the temperature change expected solely as a result of changes in drum pressure.
Claim 9
Independent Claim
112 words
A method for controlling the temperature of the steam at the outlet of the superheater of a drum type boiler operating in the sliding pressure mode, comprising the steps of: automatically controlling the fluid distribution or the heat distribution in the boiler in response to the deviation of outlet temperature from its set point so as to tend to maintain said outlet temperature at its set point; and modifying said control in response to the magnitude of a feedforward signal proportional to the pressure of the steam in said drum, said modification being in sense to tend to reduce the temperature change expected solely as a result of changes in drum pressure.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1983-12-30 | 1984-06-30 | 1984-12-30 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-12-30 | 1988-06-30 | 1988-12-30 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-12-30 | 1992-06-30 | 1992-12-30 | $7700.00 | Window Closed / Lapsed |